Process for making ethylene homopolymers
View Patent ↗A process for making an ethylene homopolymer in the presence of an oxide-supported chromium catalyst is disclosed. A small amount of an α-olefin contacted with the catalyst before polymerizing ethylene or introduced into an ethylene homopolymerization unexpectedly boosts process productivity. When used at part per million levels, the α-olefin improves productivity while maintaining desirable polymer properties. The invention is particularly valuable for making HDPE resins useful for blow molding applications.
1. A process comprising polymerizing ethylene in a reactor in the presence of an oxide-supported chromium catalyst, a diluent, and an a-olefin to produce an ethylene homopolymer; wherein the α-olefin is used in an amount effective to increase the productivity of the process compared with the productivity of the process when performed in the absence of the α-olefin.
2. The process of claim 1 wherein the oxide-supported chromium catalyst is contacted with the a-olefin prior to introducing ethylene into the reactor.
3. The process of claim 1 wherein the α-olefin is added to the reactor during the polymerization.
4. The process of claim 1 wherein the α-olefin is selected from the group consisting of propylene, 1-butene, isobutylene, and mixtures thereof.
5. The process of claim 1 wherein the α-olefin is used in an amount within the range of 1 to 500 ppm based on the amount of diluent.
6. The process of claim 1 wherein the catalyst further comprises at least one element selected from the group consisting of boron, phosphorus, aluminum, vanadium, titanium, fluorine, and zirconium.
7. The process of claim 1 wherein the productivity increase is at least 10%.
8. The process of claim 1 wherein the oxide is selected from the group consisting of silicas, silica-aluminas, aluminas, zirconias, titanias, borias, magnesias, aluminum phosphates, and mixtures thereof.
9. The process of claim 8 wherein the oxide is a silica.
10. The process of claim 1 wherein the reactor is a gas-phase or a slurry-loop reactor.
11. The process of claim 1 wherein the ethylene homopolymer has a melt index within the range of MI 20 =5 g/10 min, to MI 2 =10 g/10 min, and a density of at least 0.96 g/cm 3 .
12. A process comprising polymerizing ethylene in a slurry-loop reactor in the presence of a silica-supported chromium catalyst, a volatile aliphatic hydrocarbon diluent, and an a-olefin selected from the group consisting of propylene, 1-butene, and isobutylene, to produce an ethylene homopolymer; wherein the α-olefin is used in an amount within the range of 1 to 500 ppm based on the amount of diluent.
13. The process of claim 12 wherein the a-olefin is propylene, which is used in an amount within the range of 10 to 300 ppm based on the amount of diluent.